Pasteurizing process



April 9, 1935.

G. c. ALSTAD ET AL PASTEURIZING PROCESS 2 Shets-Sheet 1 Filed April 2, 1932 w xv? w H I N m I H April 9, 1935. s. C. ALSTAD El AL 1,997,034

PASTEUR IZING PROCESS Filed April 2, 1952 2 Sheets-Sheet 2 Patented Apr. 9, 1935- I UNITED STATES PATENT OFFICE PASTEURIZING PROCESS poration of Illinois Application April 2, 1932, serial No. 602,749

11 Claims. I This invention relates to improved dairy products and their processing to impart the desired characteristic thereto.

It contemplates more especially the processing of dairy plastics such as cheese to effect the emulsification and pasteurization thereof without body, texture and homogeneity resort to extraneous heat and/or chemicals deemed adulterants under the pure food laws and undesirable from a merchandising standpoint.

The constituents of cheese are casein and fatty oils usually termed olein which combine to form an emulsified mass or plastic having the desired smoothness of texture and taste characteristics. To avail such edibles for sale in markets remote from dairy centers-andto impart keeping qualities thereto so that handling and storage may be possible by the vendor over an interval of time within practical limits of merchandising, these are customarily pasteurized by the subjection thereof to elevated temperatures prior to packing. Pasteurization tends to preclude or at least retard deterioration occasioned by bacteria infestation responsive to natural bacteria decay over an extended period of time.

Fundamentally, the difficulty of pasteurizing cheese or other diary products with extraneous heat is the inability to prevent disintegration of theconstituents or the separation of the olein from the casein, thereby destroying the homogeneity thereof. It has long been the practice, therefore, of employing mechanical agitators and stirring ,implements during extraneous heat pasteurization to prevent or at least retard disintegration, but such expedients require skilled supervision and constant regulation not always productive of uniformity nor a firm resulting body without resort to chemicals.

As a consequence, the known processes for effecting pasteurization which require the subjection of the dairy products to heat supplied from some extraneous source, have not acquired perfection from both the standpoint of production costs and uniformity in the resulting product.

' The present invention departs entirely from known processes'in that heat of pasteurization is produced incident to the processing of dairy products to insure complete homogeneity and increased smoothness of texture without skilled supervision and regulation.

Moreover, with other widely practiced methods the constituent elements of edible dairy plastics are emulsified for complete homogeneity by the incorporation of salts like sodium citrate during the pasteurization, thereby requiring adulteration within the meaning of the pure food laws. This emulsifying salt is found necessary in known processes of pasteurizing edible substances, more particularly cheese, and in spite thereof separation of the casein from the olein will occur during the processing at or near the critical temperature.

- While pasteurization may be accomplished with the customary methods of subjecting dairy products to extraneous heat and emulsified firnmess insured or reestablished by the incorporation of chemicals such as sodium and ammonium salts of which sodium citrate and ammonium tartarateare examples, yet a vastly improved product results from processing dairy plastics without any significant disintegration or separation of the 15 constituents thereof incident thereto and without incorporating emulsifying chemicals therein. This is accomplished with the teachings of the instant invention, and the processing furthermore effects more complete emulsification and blended body firmness within controllable limits to possess good slicing qualities and 'improved taste without resort to chemicals or other undesirable substances termed adulterants. The degree of emulsification is far more pronounced than when practiced with known processes and resort to chemicals and viscolizers, for the olein is substantially held captive in the casein, curing of the dairy substance is effected, and in general far superior blending is accomplished than heretofore.

Blending by mere agitation and paddle mixing or viscolizing processes are not productive of .emulsification nor body firmness, but the accomplishment thereof in the presence of heat with progressive or other confinement not permitting separation or disintegration, is an efiicacious methodpf physically combining the constituents of one or more plastic products prior, subsequent or incident to the processing thereof. it may not be desired to pasteurize plastic products, but merely processing to effect or procure aging, to improve the texture, body and slicing characteristics thereof. This is of great importance in that dairy products are especially appetizing when possessing a fine velvety consistency in that such imparts a decidedly improved taste owing to the complete emulsified condition thereof which results from processing in accordance with the teachings of the present invention. The texture qualities andjuniformity thereof are enhanced even more by resort to primarily mechanical rather than thermal processing to impart an accentuated velvety emulsified consistency to the natural plastic product and uniformity by re- 'thereof by primarily physical rather than thermal influences.

Still another object is to improve dairy products by mechanical rather than. extraneous heat processing to the end of effecting complete homogeneity, emulsification and body firmness without resort to chemicals.

A further object is to produce improved edible plastics by the subjection of successive increments thereof to a progressive mechanical frictional reaction which effects the curing and emulsification of raw cheese.

A still further object is to provide an improved method for processing edible plastics to improve the texture, blend, taste andage qualities thereof without resort to adulterants or entailing much time.

Still a further object is to physically rather than thermally process edible substances to the end of better aging, curing, emulsifying and controlling body texture thereof without resort to adulterants and extraneous heat.

An additional object is to process cheese by the subjection thereof to varying degrees of molecular activity to effect a complete homogeneous and emulsified state.

Additionally, an object of the present invention is to provide a novel process of controlling the texture, body firmness and curing qualities of plastic substances in a continuity of uninterrupted steps.

Other objects and advantages will appear from the following description of an illustrated embodiment of the present invention.

In the drawings:

Figure 1 is a side view in elevati'onof a device capable of processing dairy products in accordance with the teachings of the instant invention.

Figure 2 is a plan'view of the device shown in Figure 1.

Figure 3 is a fragmentary sectional view taken substantially along line IIIIII of Figure 2.

A process selected for illustrating the teachings of the present invention comprises the treatment of edible substances such as butter, cheese, and kindred plastics produced by churning or other customary practices. Treatment thereof is deemed proper and necessary for the purpose of changing the texture and controlling the firmness of such products prior to the consumption or confinement thereof in containers for commercial distribution, since these dairy plastics are not suitably blended, emulsified and refined for taste as well as subject to rapid deterioration without treatment or resort to re finement.

To this end, edible plastics are either taken directly from the churn or storage where aging -is permitted to impart a predetermined strength thereto or in the instance of butter to effect preserved freshness under reduced temperatures, and

then directed for physical treatment through a constriction controlled for the creation of heat within the desired limits even to the range of pasteurization should commercial practice so dictate. In the case of cheese or other hardened plastics, the mass is ground or otherwise comminuted prior to the subjection thereof to a physical pressure reaction which elevates the temperature for direct subjection to a degree dependent upon the desired treatment for aging, curing, emulsifying or other purposes.

The heat developed mechanically, in this instance incidental to the passage thereof through a constriction, effectively refines the texture of the substances during the movement thereof along a predetermined path. This may be ac- .complished by passing the edible plastics in a comminuted condition through a constriction of any type in the presence of heat preferably evolved in a consequence thereof. No particular apparatus is essential, but to clarify the disclosure, reference is directed to a structure selected merely for illustration, there being shown a frame H] of any suitable construction which is elevated from the floor or other foundation by means 0f-corner standards ll riveted or otherwise joined thereto in the customary manner as commercial practice may dictate. Cross members l2 extend between the standards I l near the base thereof to reinforce the frame structure ill in providing a rigid and non-vibrating support for instrumentalities to be hereinafter described. In order to feed edible substances along a predetermined path, a spiral screw conveyor I3 is, in this instance, journalled for rotary support in a housing M which is constructed to conform substantially in configuration therewith.

As shown, the processing housing I4 has a feeding conduit l5 which extends in a vertic lly upward direction for communication with he interior thereof to direct the substance from any suitable source of supply to the conveyor [3. In

order to enable the cheese or other substance to be supplied to the feeding conduit I5, a substantially rectangular receptacle I6 is mounted thereabove by means of standards I! which depend to the frame I0 to effect the rigid horizontal support thereof. A suitable opening corresponding in dimensional extent and contour to the interior of the feeding conduit I5 is provided in the bottom l8 of'thecreceptacle l5 for communication therewith so that a large volume of the cheese or other substance to be processed may conveniently and readily be supplied to the processing housing l4 for traverse and feeding along a predetermined path in a mannerthat will appear more clearly hereinafter.

The processing housing I has, in this instance, a cylindrical entrant portion I9 which extends longitudinally of the frame In fortermination in a frusto-conical body 20 having a cylindrical end portion 2| serving as an auxiliary cheese treatment chamber for re-emulsification or other purposes as commercial practice may dictate or shall appear more fully hereinafter. Obviously, it is necessary or at least highly desirable to remove the initial chill from the material comprising the body of the pasteurizing housing I 4 and auxiliary parts thereof so that the developed heat of processing may be produced instantaneously responsive to the passage of the cheese therethrough. To this end, it has been found feasible and effective to provide an external casing 22 which concentrically envelopes a part of the cylindrical housing portion is, 20 and the end portion '2! of the pasteurizing housing H, it being substantially larger and of corresponding configuration to define an air chamber 23 therewith. The air chamber 23 is closed at the forward end thereof and a peripheral flange 24 slidably embraces the processing housing portion l9 for adjustable application to the housing edge 25, thereby serving as an adjustable closure or valve for the air chamber 23. Air is circulated through the chamber 23 for a purpose and controlled in a manner as will appear more fully hereinafter.

The feeding conduit [5 has, in this instance, a power actuated substance feeder mechanism comprising a cylindrical shaft 26 which has reduced axial extensions 21 for journalled support in horizontally aligned apertures in confronting walls of the'feed'ing conduit I5. As shown, the shaft 26 is positioned more proximate to one side of the conduit wall l6 than the other, .it being substantially adjacent to the more proximate wall to serve as an eccentric rotary member. To this end a substantially rectangular blade 29 is slidably projected diametrically through the shaft 26 to correspond in dimensional area with the interior cross-section of the substance feeding conduit I5; consequently the rotation thereof will effect the traverse of the cheese or. other substance displaced thereon from the receptacle 5. The path of the blade 29 is governed by confronting ledges 39 preferably of predetermined cycloidal configuration, these projecting from opposed walls of the conduit l5 and the blade 29 contacts therewith so that with the rotation of the shaft 26, the blade 29 will rotate therewith and simultaneously reciprocate diametrically therethrough. The blade 29 thus serves to feed the substance along a predetermined path for processing in a manner to be hereinafter described.

The edible plastics or substances taken directly from the churn or storage where aging is permitted to impart a predetermined strength thereto or in the instance of butter to effect preserved freshness under reduced temperatures, are then directed to the hopper or entrant orifice of the conduit l5 from the receptacle I6. The substance is then subjected to a physical pressure reaction which elevates the temperature for mechanical emulsification and/or pasteurization.

' In the present embodiment mere emulsification may be effected or heat of pasteurization developed mechanically incident to the passage of the substance through a constriction or between surfaces in frictional reaction to effect emulsification during the movement thereof, along a predetermined path. This is accomplished by passing successive increments of the. substance in comminuted or plastic condition through a constriction of any type where heat may be evolved as a consequence thereof.

In order to effect the traverse of the substances through a constriction for creating heat of pasteurization incident to the traverse thereof, the

' cylindrical portion IQ of the housing I4 is provided with a conveyor, in this instance the screw conveyor I3, which is mounted upon a shaft 3| having a segregated portion 32 thereof journalled in spacedsplit bearings 33 and 34 sustained upon cross plates 35 which are secured to the top of the frame |9 in any suitable manner. The forward extremity of the shaft 3| has, in this instance, an axial bore 31 journalled on an aligned inwardly projecting stud shaft 38 which threadedly engages a central boss 39 constituting an integral portion of an end closure 49 for the open extremity 'of the processing housing 29. It is to be noted that'a wheel 4| is carried by the stud shaft 38 to enable the shaft 3| to be engaged and disengaged responsive to the. manipulation thereof which is responsible for the registry or removal of the stud shaft 38 with the axial shaft bore 31.

The closure 49 is provided with radially extending ribs 42 formed integral therewith for projection beyond the periphery thereof to define extensions 43 complemental to bifurcated clamp members 44 which are pivotally connected for extension from the lateral face. of the processing housing rim 2 thereby enabling the association and disassociation of the closure 49 responsive to the adjustment of threaded stud members 45 which engage the clamps 44. In order to maintain the closure 49 in its operating position against displacement, the studs 45 are threaded for engagement with the clamps, to. bear against the rib extensions 43, thereby securing the closure 49 against removal. It is significant to note that the conveyor l3 has a spiral groove 46 formed therein to feed the substance therealong responsive to the rotation thereof, and it has been found advantageous to pre-condition the cheese or other dairy substance by gradually increasing the density thereof during the initial traverse by gradually diminishing the depth of the feeding groove 49. This tends to densify the dairy plastic or effects the crowding thereof to the end of preheating due to further agitation action and pressure deformation.

As shown, the cylindrical conveyor |3 merges into a conical rotor 41 splined or otherwise fixed to the shaft 3| for rotation therewith in proximity to the correspondingly shaped portion 29 of the pasteurizing housing l4, thereby defining a minute constriction therebetween for the passage of the edible substance from the conveyor |3 which has the helical convolutions in. the form of a continuous spiral groove 46 in communication therewith to enable or institute the travel of the substance between the confronting surfaces 41 and 29 which are in pressure reaction through the medium of the substance confined therebetween. The extent of the constriction defined between the surfaces 41 and 29 may be modified to conform with the desired emulsifying treatment or other processing through the medium of a lever 48 which is pivoted to a verticalrod 49 supported by brackets 59 fixed to the frame ID in any appropriate manner. The lever 48 has a pin 5| extending .therethrough for attachment to the cylindric portion l9 of the housing 14, thereby effecting the reciprocable movement thereof axially along the screw conveyor l3. To this end, the housing I4 is provided with diametrically attached and horizontally aligned ledges 52 positioned both forwardly and rearwardly and these cooperate with. correspondingly shaped brackets 53 serving as complements therefor to enable the slidable adjustment of the housing 4 relative to the rotor surface 41 with its conveyor l3.

The lever 48 is rendered responsive to a rotary hand manipulated wheel 54 which is attached to a stub shaft 55 journalled inthe confronting arms 56 of a frame attached bar 51. A spur gear 58 meshes with a pinion on the shaft 55 in the customary manner, and the former is supported by a shaft 59 having a tubular link 69 in threaded engagement with the extremity thereof, the link being pivotally connected to unnecessary friction as a result of end thrust reaction' thereon. The shaft 59 rotates relative to the pivoted link 60, thereby creating comparatively small displacement ofv the housing I4 responsive to threaded reaction of the shaft threads 63 with the correspondingly-threaded 60.

Rotation of the shaft 32 which imparts corresponding rotation to the shaft 3| owing to the complemental clutch elements 65. and 66 extending therebetween, will effect the traverse of the comminuted substance along the spiral conveyor to gradually build upand densify therealong owing to the progressive lessening depth in the conveyor convolutions 46 until reaching the entrant periphery of the rotor 41 for further displacement substantially increased compression and pressure deformation about the conlcally arcuate surface thereof to cooperate with the correspondingly shaped surface 20 of the casing body or housing l4. As shown, the conical rotor portion 41 terminates in a mixing and reemulsifying chamber defined by the cylindric housing portion 2|, and this confines a continuous spiral consisting, in this instance, of a comparatively deep convolute 61 which precludes separation of the substance components and in fact serves to better and more uniformly combine them into a moreuniform and satisfactory product. In consequence thereof, continued rotation of the conical rotor portion 41 in unison with the conveyor l3 will effect the travel of the plastic substances through the constriction defined be- -tween the reacting surfaces 41 andinterior 20 of the housing M which are in frictional reaction through the medium of thesubstance therebetween for developing heat of pasteurization or at least substance emulsification responsive to the rotation of the former with respect to the latter.

The substances are thus subjected to a pressure reaction which in conjunction with the frictional contact of the relatively moving surfaces there+ with, elevates the temperature of the moving substances to a point of pasteurization of, if desired, merely sufficient to aid in mechanical emul slfication. The degree .of temperature elevation and the maintenance thereof, at a predetermined magnitude may be controlled by the distance of the surface 41 with respect to the interior surface 23 of the housing l4 responsive to adjusting or manipulating the manually operated wheel 54 as conditions may require or deem advisable. During this passage of the plastic particles, heat is developed incidental to the rotation of the rotor surface 41 which also serves to effect movement thereof to its periphery for discharge into the agitating and re-emulsifying chamber 2| to impart improved texture,. uniformity and consistency thereto. It is thus apparent that the use of extraneous heat such as steam or any other vapor or liquid thermal medium is entirely avoided, and the processing effected in a manner which imparts complete homogeneity to the resulting produce without any possible disintegration or separation of the elements or their composition.

Discharge of the substances from the constriction and thence the re-emulsifying chamber 2| is effected primarily by the centrifugal urge imparted thereto and effective thereon at the perlphery responsive to the. rotation thereof; however, any accumulation owing to the adhering character thereof, is removed by the spiral in. the form of convolute 61--fixed to the drum 68. The drum 68-is axially attached to the forward wall 69 of the rotor 41 for rotary movement therewith, thereby expelling the emulsified and/or pasteurized substance through a discharge orifice 10 formed by a spout 1| which integrally extends from the. closure 40 for communication with the interior of the chamber 2|, a suitable gate comprising, in this instance, a slidable closure 12 is adjustably disposed in suitable guides 13 for passage through the discharge spout H to govern the flow of the substance therethrough for placement in any suitable container from a spout extension 14 which has another separately controlled slide valve 15 flanged for connection to the extremity thereof.

A lever 16 is pivoted to the housing closure 40 as at 11,"and a link 18 is interposed between the lever 18 and gate valve 12 so as to afford the more convenient control and adjustment thereof. Then, too, the slide valve 15 isindependently adjustable and the diminution or increase of substance passage has a substantial effect upon the temperature existent in the housing portion 41 and agitating or emulsifying chamber 2|. So that the temperature of the discharging substancemay be known and controlled, a thermometer 19 is suitably mounted or attached to an instrument board 80, it being in operative thermal connection to the chamber 23 of the air housing 22 to designate the temperature thereof. Similarly, a thermometer lead is attached to the discharge spout H for communication with the in,-

terior 10 thereof so that the temperature of the issuing or emulsified products may be known and controlled to produce the best and most effective result from the standpoint of homogeneity, emulsification and/or the keeping quality of the resulting product.

. The various instrumentalities necessary for effecting the emulsification and processing without resort to extraneous heat are operated from a single source of power, in this instance an electric motor 84" supported beneath the frame It for attachment thereto in any appropriate manner to prevent displacement. The armature shaft 85 of the motor 84, carries a pinion 86 which meshes with a silent chain 81 to connect a sprocket 88 fixed for rotation in unison with a stub shaft 89 journalled in bearings 90 and carried by the frame l0. A sprocket wheel 9|. is fixed to the shaft 89 between the bearings 90 thereof to drive a chain 92 which meshes with a sprocket wheel 93 fixed to the shaft 32 to effect the rotation thereof in a counterclockwise direction (viewed from the front of Figure 2) In consequence thereof, corresponding movement or rotation is imparted to the conveyor 3 and the rotor surface 41 which are fixed to the shaft 3| in operative connection with the shaft 32 by virtue of the clutch 6566 disposed therebetween. In order to simultaneously rotate the feeder blade 29- with its shaft 26 in timed relation with the conveyor l3, a shaft 94 is journalled in bearings 95 (Figure 2) fixed to the frame l0 by means of suitable fasteners,'the shaft 94 extending for a greater portion of the frame Hi to operate various instrumentalities as will appear more fully hereinafter.- A sprocket wheel 91 is fixed to the shaft 32 to establish an operative connection therewith owing to an intervening chain 98.

As shown, the shaft 94 terminates in a sprocket mounted on the extremity of the feeder blade shaft 26. A chain I05 is interposed therebetween to mesh with the sprockets I03 and I04, the sprocket I02 being operatively connected to a sprocket I06 carried by the shaft 94 through the medium of a chain I01. It will thus be apparent that the instrumentalities thus far described are motivated from a single source of energy or power, in this instance the electric motor 84. It is well known to incorporate chemical preservatives and/or flavors such as pimento in dairy or other edible substances prior or during their pasteurization. To this end, a chemical and/or flavor receiving hopper I08 of standard construction and design is mounted upon a casing I09 which is supported by inclined brackets IIO adjacent to the mixing chamber 2I and above the frame I 0. So that the various propelling, mixing and even comminuting elements or devices III thereof may discharge the desired elements along a conduit or pipe H2 in communication with the interior of the reemulsifying chamber 2|, discharges of the resulting product to the entrant orifice thereof and to control and regulate the volume of substance incorporated in the cheese or other processed substances to acquire the desired uniformity in the resulting product, the propelling,

and mixing instrumentalities III journalled in the hopper casing I09 is rendered operative responsive to the rotation of the conveyor I3.

In consequence thereof, a sprocket wheel I I3 is mounted on the shaft extremity 94 in alignment with a sprocket II4 fixed to a stub shaft II5 operatively geared to the conveying instrumentalities III journalled in the casing I09. A chain II6 extends between the sprockets H3 and I I4 in meshing engagement therewith so as to rotate the shaft H5 and impart rotation to the shaft carrying the propelling or feeding instrumentality I II in the casing I09. As a result, the chemical or other ingredient feeding device II I is operated responsive to the motor 84 which controls the movement of the other instrumentalities described, supra, in connection with the emulsifying, pasteurizing and re-emulsifying of the substances, this constituting one of the primary features of the instant invention. The relative speed of rotation of the conveyor shaft 3|, the feeder shaft 26 and the pimento feeder instrumentality III is controlled and capable of variation by virtue of the relative sizes of sprockets 93, I02, I04, I06, and H4 which may be independently changed and substituted to effect the proper relative speeds that are productive of the best results.

As stated supra, a suitable cooling medium such as air is circulated through the chamber 23 defined by the exterior casing 22. To this end, a pipe line I" establishes communication therewith along the forward lower region thereof as at I I8, and a discharge passage -I I9 extends from the rearward lower 'region for communication therewith as at I20 to establish a circuitous path for the cooling medium. The pipe line II'I terminates in a blower I2I which has a pipe I22 in communication .with the entrant orifice thereof. The pipe I22 connects with an air control chamber I23 which is closed on all sides except the end region I24. The discharge pipe 9 terminates in the air control casing I23 just forwardly of the open end I24 thereof so as a support is established between the entrant and discharge pipes II! and H9 through the casing I23.

A partition I25 is disposed intermediate the ends of the casing I23 to cooperate with a pivotal valve I26 mounted therein. The valve I26 is rendered responsive to a length I21 which connects another valve I28 pivoted along the bottom of the chamber I23 to open or close an orifice I29 provided therein. It will thus be apparent that the pivotal valves I26 and I28 are of similar size and construction, and these operate in corresponding timed relation so as to open the partition I25 when the orifice I29 closes and vice versa. "A rod I30 connects the valve I28 with an air responsive diaphragm I3I so as to manipulate and regulate the valves or dampers at I26 and I28 responsive to predetermined air pressures. An electric heater I32 is positioned approximate to the open end I24 of the air control chamber I23 so that the entrance of air therethrough responsive to the operation of the blower I2I will simultaneously energize the electric heating element I32 to warm the air that may pass therethrough for charging the chamber 23 around the cheese housing I4 through the conduit I".

An air compressor I33 is mounted on the base of the frame I0 for operation responsive to a suitable electric motor.- An air tank or reservoir I34 is in communication with the air compressor I33 to supply air through a tube (Figure 1) leading to a thermal controlled device mounted on the instrument board 80. Another tube I35 is in communication with the temperature responsive device which communicates with an air operated electric switch control (not shown) mounted on the frame I0 in a manner more fully described in my copending application serially numbered 602,748 and filed April 2,

1932. The tube also has a branch thereof con-- nected to a pressure responsive diaphragm I3I (Figure 1) through various control devices not shown herein nor necessary to elaborate there- ,control system thereby assuring the operation thereof to control the flow of air through the chamber 23 in effecting very sensitive regulation of the temperature to which the cheese or other substance is subjected. In consequence, the fiow of air through the chamber 23 defined by the housing I4 and the exterior casing 22, is regulated automatically to issue either cold or hot air therethrough depending on whether such is-introduced through the orifice I29 or the open end I24 of the control casing I23.

Various changes may be made in the embodiment of the invention herein specifically described without departing from or sacrificing any of the advantages thereof as defined in the appended claims.

We claim:

1. A method of continuously emulsifying plastic dairy products which consists in subjecting the substances to a frictional pressure reaction culminating heat of pasteurization, and then further emulsifying the substances subsequent to the pasteurization thereof.

2. A method of continuously emulsifying plastic dairy substances which consists in effecting the passage thereof between relatively moving surfaces exerting a pressure thereon, effecting pasteurization by the subjection thereof to the heat culminating therefrom, and further emulsifying the substance subsequent to pasteurization.

3. A continuous method of aging and imparting body to plastic dairy substances which consists in the confinement of increments thereof under pressure resulting in an elevated temperature within a pasteurizing range for accumulation into a uniformly blended mass, and further agitating said mass to impart increased miscibility between the constituents of the substance prior to discharge.

4. A continuous method of imparting body to plastic dairy substances which consists in the confinement of increments thereof under pressure resulting in an elevated temperature for accumulation into a uniformly blended mass,

and further agitating said mass without temperature elevation for further emulsification.

5. A continuous method of imparting body to plastic dairy substances which consists in the confinement of increments thereof for traverse along a predetermined path under pressure resulting in an elevated temperature within a pasteurizing range for accumulation into a uniformly blended mass, and then further agitating said mass without any heat development to effect the further emulsification thereof.

6. A continuous method of imparting body to plastic dairy substances which consist in the confinement of increments thereof for traverse along a predetermined path under pressure resulting in an elevated temperature within a pasteurizing range for accumulation into a uniformly blended and emulsified mass, and then continuing the traverse of said mass along a circuitous path to effect further emulsification.

7. A continuous method of imparting body to plastic dairy substances which consists in the confinement of increments thereof for traverse along a predetermined path under pressure exerted by surfaces in contact therewith with consequent temperature elevation for accumulation into a uniformly emulsified and blended mass, and then continuing the agitation of the mass for further emulsification without any further heat generation.

8. A continuous method of imparting body to plastic dairy substances which consists in the confinement of increments thereof for traverse along a predetermined path under pressure resulting in an elevated temperature within a pasteurizing range exerted by surfaces in relatively moving contact therewith for emulsified accumulation into a-uniformly blended mass, and then effecting the agitation of the mass without sub-. jection to any pressure or heat elevation for further emulsification.

9. A continuous method of imparting body to plastic dairy substances which consists in the confinement of increments thereof for traverse along a predetermined path under pressure exerted by surfaces in' relatively moving contact therewith resulting in elevated temperatures within a pasteurizing range for emulsified accumulation into a uniformly blended mass, and then continuing the agitation without consequent temperature elevation or pressure confinement for effecting further emulsification.

10. A continuous method of refining edible plastic dairy substances which consists in blending the constituents thereof under pressure, causing the traverse thereof responsive thereto along a predetermined path for extrusion from a constriction resulting in an elevated temperature, continuing the agitation of the substances without consequent heat generation or pressure confinement for further emulsification thereof, and effecting the discharge thereof for accumulation into a more dense and firm mass possessing uniform and completely emulsified characteristics.

11. A continuous method of emulsifying plastic dairy products which consists in feeding edible substances along a predetermined path, gradually densifying the substances during their traverse along said path for pre-heating purposes, subjecting said substances to a frictional pressure reaction during movement along said path to efiect'the emulsification and consequent conversion into a flowable state, and then effecting the traverse of the resulting product along a circuitous path to impart further agitation thereto for improving the texture of the substances.

- GEORGE C. ALSTAD.

JOHN H. BAUMGARTNER. 

